WO1999031179A1 - Polysiloxane renfermant un copolymere disperse et agents d'etancheite contenant ce polysiloxane - Google Patents

Polysiloxane renfermant un copolymere disperse et agents d'etancheite contenant ce polysiloxane Download PDF

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Publication number
WO1999031179A1
WO1999031179A1 PCT/US1998/025988 US9825988W WO9931179A1 WO 1999031179 A1 WO1999031179 A1 WO 1999031179A1 US 9825988 W US9825988 W US 9825988W WO 9931179 A1 WO9931179 A1 WO 9931179A1
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Prior art keywords
weight
copolymer
polysiloxane
percent
sealant
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PCT/US1998/025988
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English (en)
Inventor
Wei-Yeih Yang
Melvin Dale Beers
Tai-Min Feng
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The B.F. Goodrich Company
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Priority to JP2000539090A priority Critical patent/JP2002508426A/ja
Priority to EP19980962952 priority patent/EP1040165B1/fr
Priority to BR9813632A priority patent/BR9813632A/pt
Priority to CA 2314959 priority patent/CA2314959C/fr
Priority to AU18077/99A priority patent/AU751067B2/en
Priority to DE69806056T priority patent/DE69806056T2/de
Priority to AT98962952T priority patent/ATE219125T1/de
Priority to KR1020007006632A priority patent/KR20010024737A/ko
Publication of WO1999031179A1 publication Critical patent/WO1999031179A1/fr
Priority to NO20003136A priority patent/NO20003136L/no

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L83/00—Compositions of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon only; Compositions of derivatives of such polymers
    • C08L83/04—Polysiloxanes
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04—Polysiloxanes
    • C08G77/14—Polysiloxanes containing silicon bound to oxygen-containing groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04—Polysiloxanes
    • C08G77/20—Polysiloxanes containing silicon bound to unsaturated aliphatic groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/04—Polysiloxanes
    • C08G77/22—Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen and oxygen
    • C08G77/26—Polysiloxanes containing silicon bound to organic groups containing atoms other than carbon, hydrogen and oxygen nitrogen-containing groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
    • C08G77/70—Siloxanes defined by use of the MDTQ nomenclature
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00—Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/02—Organic macromolecular compounds, natural resins, waxes or and bituminous materials
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/31504—Composite [nonstructural laminate]
    • Y10T428/31652—Of asbestos
    • Y10T428/31663—As siloxane, silicone or silane

Definitions

  • the present invention relates to a low temperature flexible, water-repellant polysiloxane containing copolymer particles dispersed therein. More specifically, the present invention relates to the copolymer particles being formed in si tu by polymerizing at least two different types of monomers in the polysiloxane which is curable at low temperatures; for example, an ambient temperature, upon exposure to moisture. Cured sealants containing the copolymer-polysiloxane have high elongation properties.
  • Curable polyorganosiloxane also known as silicone compositions have been used as sealants, caulks, adhesives, and in other similar applications because of their excellent water repellency, good adhesion, chemical and biological inertness, and good weather resistance.
  • Such compositions generally contain a reactive polyorganosiloxane, crosslinking agents, and crosslinking catalysts.
  • Polyorganosiloxane compositions are, however, relatively expensive and do not always provide satisfactory physical properties such as toughness and strength.
  • various inorganic filler materials such as silica, diatomaceous earth, calcium carbonate, iron oxide and the like have been added.
  • U.S. Patent No. 4,138,387 to Bluestein relates to a polyolefin filled-organo polysiloxane composition which are allegedly stable dispersions comprised of a continuous phase of essentially ungrafted organo polysiloxane and a discontinuous phase of finely divided solid particles of a homopolymer or copolymer prepared from an organic monomer or monomers.
  • the composition is generally unacceptable as a sealant inasmuch as it has low elongation such as a maximum of only about 190 percent.
  • Curable dispersed copolymer-polysiloxane compositions are prepared by the in si tu free radical polymerization in a polysiloxane fluid of at least two different classes of monomers, e.g. a first class of monomers which are capable of forming a polymer having a low Tg and a second class of monomers which are capable of forming a polymer having a high Tg.
  • the copolymer which can be either a thermoplastic or a thermoset, is generally a dispersed phase in the form of particles, the surface thereof generally having substantially high Tg polymers.
  • the use of small amounts of a thixotrope renders the dispersed copolymer polysiloxane composition non-slump.
  • the composition is generally viscous and is moisture curable. Utilization of the two different classes of monomers yields synergistic results upon cure in that the dispersed copolymer-polysiloxane composition has very high elongation as well as a 100% modulus of less than 50 psi. The composition also exhibits good flexibility and excellent weathering. Unlike previous reinforcing filler technology, the in situ polymerized particles have the unique characteristics of both reinforcing (strengthening) as well as plasticizing (increasing elasticity) the cured silicone network. Another attribute of the composition of the present invention is that they have good viscosity aging resistance before cure. Accordingly, the composition is suitable for use as a binder in caulks and sealants.
  • the dispersed copolymer-polysiloxane compositions of the present invention are generally made by reacting two or more different monomers in the presence of a polysiloxane fluid.
  • the polysiloxane fluid generally contain a total of two or more reactive functional groups on the polymer chain, preferably at the terminal portion thereof.
  • the polysiloxane fluid desirably is an organo polysiloxane of the formula
  • R 1 and R 2 independently, is an alkyl having from 1 to 8 carbon atoms, desirably from 1 to 4 carbon atoms with methyl being preferred, or is an aromatic group or substituted aromatic group having from 6 to 10 carbon atoms with phenyl being preferred, and "n" is such that the weight average molecular weight of the polysiloxane is from about 2,000 to about 200,000 and desirably from about 15,000 to about 80,000 grams/mole. It is to be understood that the above polymers also contain, as noted above, two or more reactive functional groups (X) therein.
  • the functional groups independently, can be OH, or OR 3 , or N(R 4 ) 2 , or
  • R 3 through R 12 are, independently, an alkyl having from about 1 to about 8 carbon atoms .
  • the amount of the functional groups, i.e. m, is 1, 2, or 3.
  • the one or more R groups independently, is an alkyl having from 1 to 8 carbon atoms or an aromatic or an alkyl-aromatic having from 6 to 20 carbon atoms and optionally containing one or more functional groups thereon such as amine, hydroxyl, etc.
  • a polysiloxane fluid can furthermore contain a blend of two or more different polysiloxanes and/or polysiloxanes having different viscosities.
  • the polysiloxanes are generally a viscous liquid and are commercially available, e.g. Masil" SFR 6,000 from PPG Corporation and acker 6LV from acker Corporation.
  • the organopolysiloxane fluid generally constitutes a reactive continuous phase containing a discontinuous phase therein which comprises copolymer particles made in situ by free radical polymerization.
  • a reactive continuous phase containing a discontinuous phase therein which comprises copolymer particles made in situ by free radical polymerization.
  • two or more, and preferably two types of monomers are utilized wherein one, if homopolymerized, forms a low Tg polymer and the other, if homopolymerized, forms a high Tg polymer.
  • the copolymer can either be a thermoplastic, or if crosslinked, a thermose .
  • the one or more monomers utilized which otherwise would form a polymer having a low Tg, i.e. generally from about -70°C to about 0°C and desirably from about -55°C to about -10°C, include the various alkyl acrylates, and the like.
  • the alkyl acrylate monomers generally have an alkyl portion which contains from 1 to 18 carbon atoms, and desirably from 1 to 8 carbon atoms.
  • Suitable acrylates include methyl acrylate, ethyl acrylate, propyl acrylate, isopropyl acrylate, n-butyl acrylate, isobutyl acrylate, 1 -ethyl propyl acrylate, 1-methyl pentyl acrylate, pentyl acrylate, hexyl acrylate, 2-ethylhexly acrylate, and the like, with n-butyl acrylate being highly preferred.
  • a small amount of approximately 20 percent or less and desirably from about 2 to 8 percent by weight of the various alkyl acrylates can contain functional groups thereon.
  • Such groups include hydroxyl , epoxy, acetoacetyl, acrylamide, and the like, are preferably terminal groups and serve to improve adhesion to various substrates such as metals, concrete, wood, etc.
  • One or more monomers are also utilized which otherwise would form a polymer having a high Tg, i.e. generally from about 1°C or 5°C to about 150°C and desirably from about 20°C to about 120°C.
  • Such monomers include vinyl esters, acrylonitrile or derivatives thereof, vinyl substitute aromatics, alkyl methacrylates , vinyl chloride, vinylidene chloride, and the like.
  • the non-vinyl portion of the vinyl ester generally contains a total of from 2 to about 10 carbon atoms, desirably from about 2 to about 8 carbon atoms with acetate, i.e. vinyl acetate, being highly preferred.
  • acetate i.e. vinyl acetate
  • alkyl derivatives thereof containing from 1 to about 6 carbon atoms such as methyl acrylonitrile, ethyl acrylonitrile, etc. can also be utilized.
  • the vinyl substituted aromatics generally contain from 8 to about 12 carbon atoms and specific examples include styrene, alpha-methyl styrene, vinyl toluene, and the like .
  • the alkyl methacrylates include monomers wherein the alkyl group contains from 1 to 18 carbon atoms, and desirably from 1 to 8 carbon atoms. Specific examples include methyl methacrylate, ethyl methacrylate, propyl methacrylate, isopropyl methacrylate, n-butyl methacrylate, ethyl hexyl methacrylate, and the like, with methyl methacrylate, being preferred.
  • the vinyl esters are preferred, such as vinyl acetate inasmuch as it has a reactive ratio with the various acrylate monomers such that a large portion of the vinyl acetate monomers polymerize after the various acrylate monomers have polymerized.
  • the copolymer particles are generally formed by polymerization at the same time, for example, simultaneously, the low Tg polymer forming monomers and the high Tg polymer forming monomers in the presence of the organopolysiloxane fluid.
  • the type of copolymer will generally depend upon the reactivity ratios of the particular monomers. Reactivity ratios are defined in the Polymer Handbook, second edition, by J. Brandrup and E. H. Immergut, editors, 1975. If the amount and reactivity ratios of the monomers is decidedly different, the copolymers formed will initially be rich in the more reactive monomer until the more reactive monomer is consumed. Then the resulting copolymer portion formed will subsequently or terminally be rich in the less reactive monomer.
  • the reactivity ratios are similar, a random copolymer will generally be formed. Moreover, if the high Tg polymer forming monomer has a reactivity ratio similar to that of the low Tg polymer forming monomer, it is then desirable to add a large portion of the high Tg polymer forming monomer in a second or subsequent stage so that the copolymer particles be surface rich in the high Tg polymer.
  • the weight of high Tg polymer forming monomers can vary from about 2.5 percent to about 50 percent and desirably from about 20 percent to about 40 percent by weight (based upon the total weight of monomers, i.e. high and low forming the copolymer particles) .
  • the copolymer particles have a majority or are phase rich on the surface thereof with repeat units in the copolymer and/or homopolymers derived from high Tg monomers .
  • One manner of forming such particles is to add a significant amount such as from about 50 to about 100 percent by weight (i.e. from about one-half to all) of high Tg forming monomers during a late stage or a second stage of the polymerization.
  • late stage or second stage polymerization it is meant that some or most of the high Tg forming monomers are added after a certain or specified amount, for example, at least about 60 percent, desirably at least about 70 percent, and preferably at least about 80 percent of the previously added monomers (e.g. mostly low Tg forming monomers) have been polymerized.
  • the surface composition of the dispersed thermoplastic copolymer particles have a high Tg, e.g. greater than about 5°C and preferably greater than about 20°C. Otherwise viscosity aging sensitivity would often render the polysiloxane composition generally unsuitable for non-slump sealant applications.
  • Whether the surface Tg of the copolymer particles have a desired high Tg can be determined by the use of various methods or apparatus such as by atomic force microscopy, through the use of solid state nuclear magnetic resonance or through ESCA, i.e. electron spectroscopy for chemical analysis.
  • the interior of the dispersed copolymer particles should not exceed a Tg of zero degrees centigrade and desirably not above minus 10°C.
  • the dispersed phase contains copolymer particles predominantly having high Tg polymers on the surface thereof and low Tg polymers in the interior thereof .
  • the surface of the particles need not contain solely the high Tg polymer thereon and the same may exist as a partial coating, as particles, aggregates, etc., thereon, and the like.
  • the dispersed phase will at times contain small amounts of the organopolysiloxane or grafted polyorganosiloxane therein.
  • the continuous organopolysiloxane phase can contain some high and/or low Tg polymer-grafted polysiloxanes therein.
  • the shape of the dispersed copolymer particles can vary but generally is spherical or nearly spherical with the size thereof ranging from about 5 or 10 microns up to about
  • the size distribution of the dispersed particles is usually not monodisperse .
  • the weight percent of the discontinuous phase i.e. the phase containing substantially copolymers, e.g. copolymers derived from one or more high Tg forming monomers, and one or more low Tg forming monomers is from about 10 or 20 to about 85 percent and preferably from about 50 to about 75 percent by weight based upon the total weight of the discontinuous phase and the continuous polysiloxane phase .
  • the utilization of the dispersed copolymer particles having a surface Tg of at least 5°C and preferably at least 20°C and a lower Tg interior in a polysiloxane fluid unexpectedly yields a composition which has good viscosity aging resistant properties. That is, upon standing at ambient temperature, the viscosity increase of the dispersed copolymer-polysiloxane composition before cure is little or small. Thus, the compositions do not have a viscosity increase such that they become an elastic material.
  • Suitable viscosity aging properties include an increase of viscosity of generally less than 100%, desirably less than 50%, and preferably less than 25%, after aging for 24 hours at ambient temperature, i.e. 20°C, in accordance with ASTM D2452-75.
  • the dispersed copolymer-polysiloxane composition of the present invention also has unexpectedly been found upon cure to yield high elongations at break, such as at least 300 percent or 400 percent, desirably at least 500 or 600 percent, and preferably at least 700 or 800 percent up to about 1,100 percent at 20°C. Moreover, the 100% tensile strength modulus is from about 10 to about 50 psi.
  • the copolymer forming monomers are polymerized in the presence of a free radical initiator. Desirably, various initiators are utilized which are soluble in the monomers such as azo and desirably organic peroxide initiators .
  • organic peroxides examples include benzoyl peroxide, 2 , 4-dichlorobenzoyl peroxide, dialkyl peroxides such as di -tertiary-butyl peroxide and dicumyl peroxide; hydroperoxide and decylene hydroperoxide ; cyclic peroxides such as 1 , 5-dimethylhexane-l, 5-peroxide ; peresters such tert-butylperbenzoate, tert-butyl-peroxy isopropyl carbonate, tert-butylperoctyate and tert-butylperacetate.
  • azo compounds include azobisisobutyronitrile, 2, 2 -azobis-2 , 4-dimethylvaleronitrile, 2-carbamoyl, azoisobutylonitrile, dimethyl-2 , 2 ' -azobisisobutylate and 1, 1-azobiscyclohexane carbonitrile .
  • various persulfates are not utilized inasmuch as they are aqueous catalysts and are not soluble in the copolymer forming monomers of the present invention.
  • the amount of the initiators is generally from about 0.05 to about 5.0 parts by weight for every 100 parts by weight of all of the low Tg and high Tg polymer forming monomers .
  • the polymerization temperature will vary depending upon the particular monomers utilized, but generally is from about 60°C to about 130°C and preferably from about 70°C to about 100°C in order to insure a quick reaction.
  • a preferred mode of polymerization involves adding an organo polysiloxane to a reaction vessel which is free of oxygen, e.g. a nitrogen atmosphere.
  • a mixture of the two or more monomers with at least one monomer capable of forming a low Tg polymer and a different monomer capable of forming a high Tg polymer, as well as initiators, are metered into the reaction system which has previously been heated to the polymerization temperature.
  • Polymerization then occurs with the contents of the reaction vessel being mixed utilizing any conventional mixing device so that the formed copolymer particles are dispersed as a separate phase within the polysiloxane which exists generally as a continuous phase. Polymerization as well as the addition of monomers thereto is continued until a suitable amount of dispersed copolymer particles have been formed.
  • one or more crosslinking compounds having more than one polymerizable unsaturated olefinic groups such as divinyl benzene, allylmethacrylate, and the like, in amounts of up to 5 parts by weight, desirably from about 0.1 to 2 parts by weight, and preferably from about 0.1 to 0.5 parts by weight for every 100 parts by weight of the copolymer forming monomers can be used, provided that severely agglomerated or irregularly shaped particles are not formed in amounts sufficient to render the dispersion too viscous or unstable.
  • a thixotropic agent such as generally less than 3 parts by weight, desirably from about 0.05 to about 2 parts by weight, and preferably from about 0.05 to about 0.5 parts by weight per 100 parts by weight of the dispersed copolymer-polysiloxane composition.
  • suitable thixotropic agents include hydrogenated castor oil, fumed silica, precipitated calcium carbonate, and the like.
  • the above-noted amounts of thixotropic agents result in a non-slump composition, i.e. non-sagging in vertical joints as measured by ASTM D 2202- 938.
  • the dispersed copolymer-polysiloxane compositions of the present invention are cured by generally subjecting them to moisture.
  • Either a conventional one-component or two-component cure system can be utilized.
  • the polysiloxane is converted to a compound having an alkoxy, an oxime , an enoxy, an amido, an amino, or an acetoxy blocking group in a manner well known to the art and to the literature.
  • the blocked one-component cure system can contain crosslinking agents as set forth herein below.
  • crosslinking agents such as a multi-functional alkoxy silane or oligomers thereof and catalysts are kept separate from the polysiloxane until reaction.
  • the amount of catalyst for the two component system is generally much higher than in the one component system.
  • Such cure systems are well known to the art, e.g. see Rubber Technology, 3rd Edition, pp. 406-07, 1987, by Maurice Morton, Van Nostrand Reinhold, which is hereby fully incorporated by reference.
  • oxime crosslinkers are preferred, such as for example, vinyl tris-methylethylketoximosilane , and methyltris-methylethylketoximosilane .
  • Methyltris- methylethylketoximosilane (MOS) is available under the trade name OS-1000 from Allied Signal Corp.
  • crosslinkers are also suitable; such as for example, alkoxysilanes, epoxyalkylalkoxysilanes , amido silanes, aminosilanes, enoxysilanes and the like, such as tetraethoxysilanes, methyltrimethoxy silane, vinyl trimethoxysilane, glycidoxypropyltrimethoxsilane , vinyl tris -isopropenoxysilane, methyl tris-isopropenoxysilane, methyl tris-cyclohexylaminosilane, and methyl tris- secondarybutylaminosilane .
  • Mixtures of crosslinkers can also be employed.
  • the amount of the crosslinking agent is generally from about 0.2 to about 20 parts by weight, desirably from about 1 to about 10 parts by weight, and preferably from about 1.5 to about 6.5 parts by weight for every 100 parts by weight of said copolymer-polysiloxane.
  • compatibilizing agents are optionally utilized to generally form a thin layer which compatibilizes the generally otherwise incompatible polysiloxane with a dispersed high Tg-low Tg polymer phase and thus helps control the particle size, improve tensile strength properties, and result in lower dispersion viscosities.
  • Suitable compatibilizing agents include vinyl containing or mercapto containing polyorganosiloxanes, or macromonomers such as monomethacryloxypropyl terminated polydimethylsiloxane, and the like, with vinyl terminated polydimethyl siloxane such as PS443 from United Chemical Technologies, Inc. being preferred.
  • the amount of the optional compatibilizing agents are generally up to about 15 parts by weight, and desirably from about 1 to about 5 parts by weight for every 100 parts by weight of the high and low Tg polymer forming monomers .
  • the dispersed copolymer-polysiloxane composition generally has a low viscosity which permits it to be readily extruded.
  • the copolymer-polysiloxane can be used in low temperature applications.
  • the composition Upon exposure to moisture, the composition cures and forms a low temperature flexible, water repellant, thermal oxidative resistant, UV resistant material.
  • the composition also upon cure has low shrinkage and is soft and pliable.
  • the dispersed copolymer-polysiloxane composition has synergistic elongation properties at break as noted above of from about 300 to about 1,100 percent and yet has low 100% tensile modulus properties, the combination of which is highly desired for sealant properties.
  • Sealant compositions which are particularly useful as caulks, are comprised of the dispersed copolymer- polysiloxane, one or more of the above noted crosslinkers, and optionally though preferably: an adhesion promoter; a reinforcing agent; a chain extender; and a plasticizer.
  • the sealants in their uncured states have little sag, generally less than about 1.0 inches, desirably less than about 0.5 inches, preferably less than about 0.2 inches, most preferably about 0.
  • the uncured sealants are easy to tool and have a tooling life of from about 5 to about 240, desirably from about 10 to about 180, and preferably from about 20 to about 150 minutes.
  • the sealants become tack free in generally about 0.5 to about 12 hours, desirably from about 1 to about 8 hours, and preferably from about 1.5 to about 7 hours.
  • the sealants become substantially cured, i.e. chemically crosslinked, in about 7 days although this may vary depending upon the curing system, particularly the catalyst employed.
  • the sealants are typically completely cured at about 21 days at 25°C and 50% relative humidity.
  • the cured sealant has a shore A hardness generally from about 3 to about 45, desirably from about 8 to about 35, and preferably from about 10 to about 25; a tensile strength generally from about 20 to about 400, desirably from about 50 to about 300, and preferably from about 60 to about 200 psi; an elongation to break of generally from about 250 to about 1600, desirably from about 350 to about 1400, and preferably from about 400 to about 1200 percent; and a 100% extension modulus of generally from about 8 to about 130 psi, desirably from about 10 to about 100 psi, preferably from about 10 to about 50 psi, and most preferably from about 15 to about 35 psi.
  • the extension modulus is measured according to ASTM D412 at 100% elongation.
  • the amount of the adhesion promoter in the sealing composition is generally from 0 to about 15, desirably from about 0.3 to about 15, preferably from about 0.75 to about 6, and more preferably from about 1 to about 3 parts by weight based upon 100 parts by weight of the copolymer and polysiloxane.
  • the amount of the reinforcing agent is generally from 0 to about 100, desirably from about 0.1 to about 100, preferably from about 0.1 to about 60, and more preferably from about 0.2 to about 30 parts by weight based upon 100 parts by weight of the copolymer and the polysiloxane.
  • the amount of the plasticizer is from 0 to about 80, desirably from about 5 to about 80, and preferably from about 10 to about 30 parts by weight based upon 100 parts by weight of the copolymer and the polysiloxane.
  • the amount of the chain extender is generally from 0 to about 12, desirably from about 0.2 to about 12, preferably from about 0.2 to about 8, and more preferably from about 0.5 to about 5 parts by weight based upon 100 parts weight of the polysiloxane.
  • the plasticizer contributes to the flexibility, particularly low temperature flexibility, of the cured sealant.
  • the addition of the plasticizer unlike conventional polysiloxanes which result in reduced tensile strength, imparts improved tensile strength to the copolymer-polysiloxane admixture.
  • the plasticizer also modifies the modulus of the cured sealant; if modulus values exceed about 100 psi at 100% extension, the cured sealant tends to pull the surface of the material, particularly materials like concrete, to which the sealant is applied.
  • the modulus values of the cured sealant are preferably less than about 60 psi, more preferably less than about 40 psi.
  • the plasticizer generally has a number average molecular weight of from about 100 to about 800 and desirably from about 200 to about 400. Preferably the plasticizer has a boiling point greater than about 100°C, at 1 atmospheric pressure.
  • Suitable plasticizers are phthalate esters, dibenezoate esters, phosphate esters, and adipate esters. Examples of phthalate esters are dibutyl phthalate, dioctyl phthalate, dimethyl phthalate, diisodecyl phthalate, butyl benzyl phthalate, texanol benzyl phthalate, C 7 benzyl phthalate, and C 9 benzyl phthalate. Examples of dibenzoate esters are dipropylene glycol dibenzoate, polypropylene gylcol dibenzoate, diethylene glycol, and triethylene glycol dibenzoate.
  • adipate esters are dioctyl adipate, ditridecyl adipate, and dialkyl adipate.
  • phosphate esters are tricryesyl phosphate, trioctyl phosphate, triphenyl phosphate, and t-butylphenyl diphenyl phosphate.
  • suitable plasticizers are for example terephthalates such as 1, 4-benzenedicarboxylates, and trimelliatics such as 1 , 2 , 4-benzenedicarboxylates .
  • a suitable butyl benzyl phthalate, a phthalate ester of butyl alcohol and benzyl alcohol, is commercially available as Santicizer 160 formerly from Monsanto Solution Company, St. Louis, Missouri, now Solutia St. Louis, Missouri.
  • the chain extenders are difunctional molecules which extend the length of the polysiloxane polymer chains and modify the modulus of elongation of the cured sealant.
  • Suitable classes of chain extenders are silane chain extenders such as amino silanes, amido silanes, acetoxy silanes, and aminoxy silanes.
  • Suitable chain extenders are for example, methylvinyl bis-N, -methylacetamidosilane, methylhydrogendiacetoxysilane , dimethylbis- diethylhydroxylaminosilane and dimethylbis- secondarybutylaminosilane .
  • Dimethylbis-secondary butylaminosilane is available under the trade name SB-72 from Wacker Silicones of Adrian, Michigan.
  • adhesion promoter although optional, is highly preferred; the adhesion promoter provides the sealant with long term adhesion to the substrate.
  • Suitable classes of adhesion promoters are aminoalkyl, mercaptoalkyl , epoxyalkyl , ureidoalkyl, carboxy, acrylate and isocyanurate functional silanes .
  • adhesion promoters examples include mercaptopropyltrimethoxysilane, glycidoxpropyltrimethoxysilane , aminopropyltriethoxysilane , aminoethylaminopropyltrimethoxysilane, ureidopropyltrimethyloxysilane , bis- ⁇ -trimethoxysilyl- propylurea, 1,3, 5-tris- ⁇ -trimethoxysilylpropylisocyanurate, bis- ⁇ -trimethoxysilylpropylmaleate and fumarate and ⁇ - methacryloxypropyltrimethoxysilane
  • a suitable silane adhesion promoter is aminopropyltriethoxysilane which is available under the trade designation A-1100 Silane from OSi, a division of Witco Corporation.
  • the reinforcing agents are optional although highly preferred, particularly when the sealant is used as a caulk. Reinforcing agents increase tensile strength in the cured sealant and reduce sag of the uncured sealant.
  • the reinforcing agent also functions as a thixotrope.
  • Such reinforcing agents are finely divided particulates and include both the conventionally known reinforcing agents and semi-reinforcing agents, typically having a particle size less than about 10 microns, preferably about 5 microns or less, more preferably about 0.1 microns or less.
  • Suitable reinforcing agents include hydrophobic treated fumed silicas, such as TS 720 from Cabot Corporation, or R- 972 from Degussa Corporation, hydrophobic precipitated calcium carbonates, talc, zinc oxides, and polyvinyl chloride powders.
  • ingredients can also be utilized in the sealant formulation in amounts up to about 20 parts by weight and desirably from about 0.01 to about 15 parts by weight per 100 parts by weight of the copolymer and the polysiloxane.
  • Such ingredients include fungicides.
  • extender fillers such as ground calcium carbonates and diatomaceous earth are optionally employed. Such extenders have minimal or no reinforcing effect and/or minimal or no thixotropic effect.
  • UV stabilizers can be optionally added.
  • Pigments or colorants such as titanium dioxide, iron oxide, carbon black are optionally employed to impart color to the sealant and/or to act as ultraviolet stabilizer. LTV inhibitors, anitozonates are also optionally added.
  • the sealant in its uncured state may optionally contain solvents such as organic solvents to reduce the viscosity; such solvents are employed where the sealant is to be used as a coating such as for a roof. Such solvents are less preferred where the sealant is to be used as a caulk since as such solvents evaporate, the cured sealant shrinks which is not desirable.
  • solvents such as organic solvents to reduce the viscosity; such solvents are employed where the sealant is to be used as a coating such as for a roof.
  • solvents are less preferred where the sealant is to be used as a caulk since as such solvents evaporate, the cured sealant shrinks which is not desirable.
  • the present invention relates to a family of silicone sealants which generally meet all of the performance features demanded by the construction industry for joint and general sealing such as; non-staining characteristics on porous substrates like white marble, virtually no change of properties during weather exposure, low modulus elastomeric behavior to accommodate joint movement without adhesive or cohesive failure, extended tooling life which allows a worker to apply the sealant in long joints before having to tool the surface of the sealant and primerless adhesion to a broad spectrum of substrates such as anodized aluminum, concrete, brick, mortar, marble, granite, limestone, porcelain, glass, painted surfaces, wood, PVC, polyacrylate, polycarbonate, and polystyrene, etc.
  • substrates such as anodized aluminum, concrete, brick, mortar, marble, granite, limestone, porcelain, glass, painted surfaces, wood, PVC, polyacrylate, polycarbonate, and polystyrene, etc.
  • the copolymer-silicone sealants of the present invention can generally have tooling times in excess of 2 hours.
  • the copolymer-silicone sealant compositions of the present invention have good low modulus characteristics such as low as 10 to 20 PSI at 100 percent extension.
  • Conventional silicone sealants generally do not have such a high elongation with extreme low modulus and can fail on weak tensile stress surfaces such as concrete.
  • the copolymer- polysiloxane compositions of the present invention can also be used to coat fabrics, or to form gaskets.
  • silicone alloys including thermoset alloys such as RTV (room temperature vulcanizable) silicone- acrylate alloys, molded silicone rubbers, and silicone- acrylate epoxy additives wherein the silicone can be the copolymer- polysiloxane composition of the present invention or it can be a mixture or blend of a conventional silicone and the copolymer-polysiloxane composition of the present invention.
  • the composition of the present invention can also be used in medical applications, electronic applications, automotive applications, textile applications, paper coatings, polishes, cosmetic applications, pharmaceutical applications and as processing aids.
  • the reactor used for polymerization was a 5-neck jacketed 2 liter resin kettle, fitted with a mechanical stirrer, a condenser, a nitrogen- inlet , a vacuum port and a safety release valve.
  • the monomer/initiator mixture was stored in a graduated cylinder, which was refrigerated and was kept under a gentle nitrogen sweep.
  • the feeding was done from the bottom of the reactor and the rate of which was controlled by a metering pump.
  • thermo-control- console monitored the temperature of the thermocouple located at the bottom of the reactor and controlled the timing of opening and closing of a diaphragm valve.
  • the diaphragm valve was installed to control the flow of the cool polysiloxane fluid into the heating loop, such that the exotherm of the polymerization could be counteracted.
  • Four additional temperature readouts updated the temperatures of reactor inlet, reactor outlet, monomer/initiator reservoir and polysiloxane bath.
  • the thermo-couple inside the reactor was located at the bottom of the resin kettle about one-half inch below the monomer inlet.
  • the agitation was accomplished by specially designed blades, which have two two-leafed marine blades, about 3 inches apart along the stainless steel shaft and two sweeping blades which keep the material on the interior wall moving.
  • two small slanted blades at the foot of each sweeping blade were also provided.
  • the speed of stirring was controlled by a variable speed electric motor. The stirring speed and the torque exerted on the stirring shaft were constantly displayed by a digital readout .
  • the weighed monomer/initiator mixture was poured into the refrigerated reservoir via a funnel. The contents were then kept under a nitrogen sweep.
  • the polysiloxane fluid was weighed and placed in the reactor.
  • the stirring speed was set at 100 rpm.
  • the reactor was evacuated to rid it of oxygen. Then, the inside temperature was brought to the desired polymerization temperature .
  • the monomer/initiator was fed into the reactor via a metering pump according to a pre-determined rate. After the monomer addition was completed, the temperature was raised to 90°C and the polymerization continued for 2 hours.
  • the final phase of the polymerization was carried out by first injecting 0.02 phr of Lupersol 575 initiator to the reactor, raising the reactor temperature to 100°C, and then starting the vacuum stripping for 1 hour.
  • the residual monomer can be effectively reduced to very low levels, either by using a high temperature- activated initiator as part of the initiator package or by using a booster shot of initiators during the final phase of the polymerization. Vacuum stripping will aid the efficiency of monomer removal.
  • polysiloxane compositions were produced from the recipes set forth in Table I, wherein the parts are by weight. TABLE 1
  • Example 1 had poor viscosity aging inasmuch as no vinyl acetate, (i.e. a high Tg forming monomer) was utilized.
  • Examples 2-5 wherein vinyl acetate was utilized which yields a very high Tg polymer, and yet has a low reactivity ratio so that it is located generally on the surface of the particles, good viscosity aging properties were obtained.
  • Example 6 Although vinyl acetate was utilized in Example 6, the amount thereof is thought not to be sufficient to form a surface rich high Tg polymer on the copolymer particle. The amount of vinyl acetate in Example 5 can be distinguished from Example 6 because additional vinyl acetate was added in a second stage in Example 5.
  • Tlie final phase of the polyinerizalion is carried out hy first injecting 0 02 phr of Lupersol 575 to the reactor, raising Ihe reaclor temperature to 100-110"C, and then start vacuum stripping for 1 hour
  • compositions formed were tested with regard to viscosity aging sensitivity and the results thereof are set forth in Table IV.
  • the flow rate and the viscosity aging sensitivity data relate to uncured compositions containing the copolymers dispersed in the polysiloxane whereas the tensile data relates to cured compositions which were cured in a manner identical to Table II.
  • compositions of Table III generally utilized a two stage polymerization wherein significant amounts of vinyl acetate was added in the second stage, thus generally resulting in a copolymer surface rich in a high Tg polymer.
  • Examples, 12, 13, and 14 which did not utilize vinyl acetate in the second stage did not have good viscosity aging properties.
  • Example 15 relates to the use of a polysiloxane composition of the present invention, i.e. Example 2, which was utilized as an additive in an epoxy coating.
  • Example 15 relates to an epoxy coating having improved toughness and water repellency.
  • the epoxy coating can be applied to various substrates such as concrete, metal, wood, and the like.
  • An acrylate terpolymer suspension was polymerized in the presence of a silanol terminated- dimethylpolysiloxane polymer, to provide a dispersed copolymer-polysiloxane composition having 70% soft acrylate polymer and 30% silanol terminated dimethylpolysiloxane .
  • a dispersed copolymer-polysiloxane composition, Example 16 was prepared from the following ingredients.
  • a monomer feed tank was charged with 102.2g of vinyl acetate, 517.6g of n-Butyl acrylate, 66.6g of methyl methacrylate, 3.3g of N-t-butyl acrylamide, and 13.7g of vinyl terminated siloxane polymer to provide a first mixture.
  • Catalyst was charged to a container with 1.47g of Lupersol 546-M75 and 0.84g of Lupersol 546-M75 to provide a second mixture. Then the first and second mixtures were fed simultaneously to the reactor over a period of about three hours at about 80°C. Then the material was aged at 80°C for 30 minutes; then chaser a was added, and the composition was aged for about 30 minutes.
  • Next chaser b was added, and the temperature was raised to about 95°C, and the composition was aged for about 60 minutes.
  • Next chaser c was added, the temperature was raised to about 110°C, and the composition was aged for about 60 minutes. Then vacuum was applied for about 30 minutes at about 110°C and then the composition was cooled to about 75°C with the vacuum on, and then the dispersed copolymer polysiloxane composition was discharged.
  • the viscosity of the resulting dispersed copolymer polysiloxane composition was about 240,000 cps as measured on an HBT Brookfiled viscosometer using a number 6 spindle at 10 rpm.
  • Example 17 was made as was Example 16, except that the N-t-butylacrylamide was not utilized.
  • a sealant composition suitable for use as a caulk was prepared using the following ingredients:
  • the dispersed copolymer polysiloxane composition of Example 16 was used to prepare the low modulus sealant composition from the above ingredients. First the fillers and reinforcing agents were incorporated into the dispersed copolymer polysiloxane composition of Example 16 under high shear mixing conditions and vacuum in a changecan mixer, before the Santicizer 160 plasticizer was added. By first adding the fillers and reinforcing agents a maximum dispersion of the fillers was achieved.
  • the dispersed copolymer polysiloxane composition- filler mixture and plasticizer were then mixed under vacuum at 100 ⁇ 5°C for two hours to remove moisture from the precipitated calcium carbonate and the ground calcium carbonate. This mixture was then cooled below 50°C, and then the moisture sensitive ingredients were added under dry nitrogen and mixed under vacuum for twenty minutes. Next the final sealant product was packaged.
  • a sealant composition suitable for use as a caulk was prepared as in example 19, except that the following ingredients were used.
  • a sealant composition suitable for use as a caulk was prepared as in example 19, except that the following ingredients were used.
  • a sealant composition suitable for use as a caulk was prepared as in Example 19, except that the following ingredients were used in the amounts listed below.
  • Tooling life was measured using a round tip spatula at 25°C and 50% humidity, according to Mil-S-8802 , sag was measured according to the Boeing sag flow in Mil-S-8802; extrusion rate was measured according to ASTM D-2254; and tack free time was measured at according to the polyethylene release using a 25 gram weight according to Mil-S-8802. Examples 15-18 did not stain porous materials such as marble and are particularly desirable for use with such porous materials. Table V Properties of Uncured Sealants
  • the sealants of examples 19-22 were coated, or more specifically drawn down, on a polyethylene sheets and cured at 25 °C and 50% relative humidity for 21 days. The materials were then released from the polyethylene and evaluated; shore A hardness was measured according to the Shore a Instrument test method according to in ASTM D-2240, tensile strength was measured using a Instron 20 inch/minute jaw separation rate according to ASTM D-412, modulus was measured using a Instron 20 inch/minute jaw separation rate according to ASTM D-412, and elongation was measured using Instron 20 inch/minute jaw separation rate according to ASTM D-412. The results are presented in Table VI.
  • the sealant of Example 19-22 all demonstrated cohesive adhesion to glass, concrete limestone, marble and anodized aluminum substrates. No shrinkage was observed.
  • suitable substrates for the sealants include, for example, plastic, particularly polyacrylate, and rigid PVC, painted surfaces, wood, metal, stone, brick and other masonry materials.

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Sealing Material Composition (AREA)
  • Paints Or Removers (AREA)

Abstract

L'invention concerne une composition à étirement élevé et à module 100 % réduit, renfermant un copolymère dispersé dans un polysiloxane à phase continue. Ce copolymère est fabriqué à partir de grandes quantités d'au moins un monomère capable de former un polymère à faible température de transition vitreuse (Tg), et de quantités relativement faibles d'au moins un monomère capable de former un polymère à Tg élevée. Le monomère constituant ce polymère à Tg élevée peut être un acrylate d'alkyle alors que les monomères formant ledit polymère à Tg élevée peuvent être un ester de vinyle, un acrylonitrile ou des dérivés de celui-ci, un aromate substitué par le vinyle tel que le styrène, un méthacrylate d'alkyle, et similaire. La composition de cette invention, qui présente une bonne adhésion aux substrats ainsi qu'un bon vieillissement de la viscosité, peut être utilisée dans des enduits ou des agents d'étanchéité.
PCT/US1998/025988 1997-12-18 1998-12-08 Polysiloxane renfermant un copolymere disperse et agents d'etancheite contenant ce polysiloxane WO1999031179A1 (fr)

Priority Applications (9)

Application Number Priority Date Filing Date Title
JP2000539090A JP2002508426A (ja) 1997-12-18 1998-12-08 コポリマーが分散されたポリシロキサンおよびそれを含有するシーリング剤
EP19980962952 EP1040165B1 (fr) 1997-12-18 1998-12-08 Polysiloxane renfermant un copolymere disperse et agents d'etancheite contenant ce polysiloxane
BR9813632A BR9813632A (pt) 1997-12-18 1998-12-08 Composição de copolìmero-polisiloxano não curada, processo para formação de uma composição de polisiloxano, selante, e, substrato revestido com selante
CA 2314959 CA2314959C (fr) 1997-12-18 1998-12-08 Polysiloxane renfermant un copolymere disperse et agents d'etancheite contenant ce polysiloxane
AU18077/99A AU751067B2 (en) 1997-12-18 1998-12-08 A polysiloxane having a copolymer dispersed therein and sealants containing the same
DE69806056T DE69806056T2 (de) 1997-12-18 1998-12-08 Polysiloxan mit dispergiertem copolymeren und dieses enthaltende dichtungsmassen
AT98962952T ATE219125T1 (de) 1997-12-18 1998-12-08 Polysiloxan mit dispergiertem copolymeren und dieses enthaltende dichtungsmassen
KR1020007006632A KR20010024737A (ko) 1997-12-18 1998-12-08 공중합체가 분산되어 있는 폴리실록산 및 이를 함유하는실런트
NO20003136A NO20003136L (no) 1997-12-18 2000-06-16 Et polysiloksan som har en kopolymer dispergert deri og tetningsmasse inneholdende samme

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US99391197A 1997-12-18 1997-12-18
US08/993,911 1997-12-18

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CN100338161C (zh) * 2003-01-30 2007-09-19 阿克佐诺贝尔国际涂料股份有限公司 室温固化的涂料组合物
US7402623B1 (en) 2004-10-06 2008-07-22 Chemmasters Inc. Composition and process for treating concrete
US7452945B2 (en) 2003-01-30 2008-11-18 Akzo Nobel Coatings International B.V. Ambient temperature curing coating composition

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AU2001279661B2 (en) * 2000-06-23 2006-07-06 International Coatings Limited Ambient temperature curing coating composition
DE10103421A1 (de) 2001-01-26 2002-08-14 Ge Bayer Silicones Gmbh & Co Polyorganosiloxan-Zusammensetzung
US7074481B2 (en) * 2001-09-17 2006-07-11 Dow Corning Corporation Adhesives for semiconductor applications efficient processes for producing such devices and the devices per se produced by the efficient processes
JP5247969B2 (ja) * 2003-12-25 2013-07-24 東レ・ダウコーニング株式会社 木用接着剤、該接着剤を用いる接着方法、並びに、該接着剤を用いた複合体
US20050288415A1 (en) * 2004-06-23 2005-12-29 Beers Melvin D Highly elastomeric and paintable silicone compositions
US7605203B2 (en) * 2005-05-26 2009-10-20 Tremco Incorporated Polymer compositions and adhesives, coatings, and sealants made therefrom
FR2886299B1 (fr) * 2005-05-26 2010-08-20 Saint Gobain Vetrotex Dispersion de polymere dans un milieu organique reactif, procede de preparation et utilisations
JP4766248B2 (ja) * 2006-02-01 2011-09-07 信越化学工業株式会社 耐薬品性に優れるマグネシウム合金接着用オルガノポリシロキサン組成物
US20070219307A1 (en) * 2006-03-17 2007-09-20 Yong Yang Emulsion polymer blend coating compositions and methods for increasing chalky substrate adhesion
JP5462769B2 (ja) * 2010-11-17 2014-04-02 東レ・ダウコーニング株式会社 木用接着剤、該接着剤を用いる接着方法、並びに、該接着剤を用いた複合体
CA2964866C (fr) 2016-04-20 2022-10-04 Owens Corning Intellectual Capital, Llc Combinaison de bardeau depart/crete et creux
US10358824B2 (en) 2016-05-06 2019-07-23 Owens Corning Intellectual Capital, Llc Shingle sealing arrangements
CN112111155B (zh) * 2019-06-19 2022-04-01 中国科学院化学研究所 一种聚甲基丙烯酸烷基酯与硅橡胶的共混聚合物材料及其制备方法和应用

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CN100338161C (zh) * 2003-01-30 2007-09-19 阿克佐诺贝尔国际涂料股份有限公司 室温固化的涂料组合物
US7452945B2 (en) 2003-01-30 2008-11-18 Akzo Nobel Coatings International B.V. Ambient temperature curing coating composition
US7402623B1 (en) 2004-10-06 2008-07-22 Chemmasters Inc. Composition and process for treating concrete

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CA2314959C (fr) 2006-10-03
CA2314959A1 (fr) 1999-06-24
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BR9813632A (pt) 2000-10-17
CN1170888C (zh) 2004-10-13
US6403711B1 (en) 2002-06-11
CN1282353A (zh) 2001-01-31
DE69806056D1 (de) 2002-07-18
AU751067B2 (en) 2002-08-08
ATE219125T1 (de) 2002-06-15
NO20003136D0 (no) 2000-06-16
JP2002508426A (ja) 2002-03-19
DE69806056T2 (de) 2003-01-23
KR20010024737A (ko) 2001-03-26
AU1807799A (en) 1999-07-05
EP1040165B1 (fr) 2002-06-12
NO20003136L (no) 2000-08-16

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